WO1998051165A1 - Milled cereal by-product which is an additive for increasing total dietary fiber - Google Patents
Milled cereal by-product which is an additive for increasing total dietary fiber Download PDFInfo
- Publication number
- WO1998051165A1 WO1998051165A1 PCT/US1998/009913 US9809913W WO9851165A1 WO 1998051165 A1 WO1998051165 A1 WO 1998051165A1 US 9809913 W US9809913 W US 9809913W WO 9851165 A1 WO9851165 A1 WO 9851165A1
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- WO
- WIPO (PCT)
- Prior art keywords
- bran
- weight percent
- starch
- product
- additive composition
- Prior art date
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Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/20—Reducing nutritive value; Dietetic products with reduced nutritive value
- A23L33/21—Addition of substantially indigestible substances, e.g. dietary fibres
- A23L33/22—Comminuted fibrous parts of plants, e.g. bagasse or pulp
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- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
- A21D13/00—Finished or partly finished bakery products
- A21D13/40—Products characterised by the type, form or use
- A21D13/42—Tortillas
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- A—HUMAN NECESSITIES
- A21—BAKING; EDIBLE DOUGHS
- A21D—TREATMENT, e.g. PRESERVATION, OF FLOUR OR DOUGH, e.g. BY ADDITION OF MATERIALS; BAKING; BAKERY PRODUCTS; PRESERVATION THEREOF
- A21D2/00—Treatment of flour or dough by adding materials thereto before or during baking
- A21D2/08—Treatment of flour or dough by adding materials thereto before or during baking by adding organic substances
- A21D2/14—Organic oxygen compounds
- A21D2/18—Carbohydrates
- A21D2/186—Starches; Derivatives thereof
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/115—Cereal fibre products, e.g. bran, husk
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L7/00—Cereal-derived products; Malt products; Preparation or treatment thereof
- A23L7/10—Cereal-derived products
- A23L7/117—Flakes or other shapes of ready-to-eat type; Semi-finished or partly-finished products therefor
Definitions
- the present invention generally relates to an additive composition effective for increasing total dietary fiber in a wide variety of food products.
- cereal grain is usually subjected to a milling process.
- the hulls (bran) and germ which are the structures rich in minerals and vitamins, are more or less completely removed.
- Refined mill products such as masa flour, consist chiefly of the endosperm.
- Portions of the corn kernel removed from the endosperm, such as the hulls or bran, are considered to be waste byproducts which are often put into animal feed.
- a maize kernel is known as a caryposis, a dry, one-seeded, nutlike berry in which the fruit coat and seed are fused to form a single grain.
- Mature kernels are composed of four major parts: pericarp (hull or bran), germ (embryo), endosperm and tip cap.
- pericarp hull or bran
- germ epiosperm
- tip cap The average composition of whole maize, and its fractions, on a moisture-free (dry) basis is as follows:
- Peri carp The maize kernel is covered by a water- impermeable cuticle.
- the pericarp hull or bran
- the pericarp is the mature ovary wall which is beneath the cuticle, and comprises all the outer cell layers down to the seed coat. It is high in non-starch-polysaccharides, such as cellulose and pentosans.
- ⁇ A pentosan is a complex carbohydrate present in many plant tissues, particularly brans, characterized by hydrolysis to give five-carbon- atom monosaccharides [pentoses] . It is any member of a group of pentose polysaccharides having the formula (C 5 H 8 0 4 ) n found in various foods and plant juices. ⁇
- the pericarp is tough.
- Germ The scutulum and the embryonic axis are the two major parts of the germ.
- the scutulum makes up 90% of the germ, and stores nutrients mobilized during germination. During this transformation, the embryonic axis grows into a seedling.
- the germ is characterized by its high fatty oil content. It is also rich in crude proteins, sugars, and ash constituents.
- the scutulum contains oil-rich parenchyma cells which have pitted cell walls. Of the sugars present in the germ, about 67% is glucose.
- Endosperm contains the starch, and is lower in protein content than the germ and the bran. It is also low in crude fat and ash constituents.
- Tip cap The tip cap, where the kernel is joined to the cob, is a continuation of the pericarp, and is usually present during shelling. It contains a loose and spongy parenchyma.
- Corn Milling In milling corn to obtain flour, the corn is first cleaned, and is then usually passed through a scourer to remove the tip from the germ end of the kernel. The corn is then tempered by the addition of water to a moisture content which is generally from about 21% to about 24%. The corn is frequently then passed through a corn degerminator, which frees the bran and germ, and breaks the endosperm into two or more pieces. The stock from the degerminator is generally dried to about 14% to 16% moisture in revolving dryers equipped with steam coils, and is then cooled in revolving or gravity-type coolers. The stock is next passed through a hominy separator, which first separates the fine particles, and then grades and polishes the larger fragments into four sizes.
- the various grades of broken corn are passed through centrifugal-type aspirators to remove any loose bran from the endosperm fragments, and produce milled cereal byproducts such as aspirated bran. These by-products are waste products which heretofore had little value.
- “Aspirated bran” from corn and other cereal grains is an impure form of whole bran which generally contains some of the floury endosperm, and the starch and protein present therein, and some germ, and the protein present therein, and may contain some grits. Generally, most of the germ and grits will already have been removed from the cereal grain at this point in the milling process. It is possible for the aspirated bran to contain no germ, to contain all of the germ, or to contain any amount of germ in between. Similarly, the aspirated bran fraction may contain no grits from the cereal grain, may contain all of the grits, or may contain any amount of the grits in between.
- Masa Flour and Dough Masa flour dry corn flour which has usually been nixtamalized
- masa corn dough which has usually been nixtamalized
- Nixtamalization is the cooking of cereal grain, such as whole corn kernels, in a medium which usually contains an alkaline agent, such as water containing lime (CaO) .
- an additive which increases the fiber content and nutritional value of products produced from the flour or dough as well as other food products by providing an additive with a higher fiber content, and with additional vitamins and minerals. Further, it would be advantageous to produce such an additive composition without the production of liquid waste with a material which is essentially a waste by- product from the milling of cereal, such as whole corn. It would also be advantageous to provide tortillas and related products prepared with such an additive which would retain the flavors and other positive attributes of tortillas and related products prepared without such additive.
- the additive of the present invention imparts the advantageous properties described above to tortillas and other food products, such as juices, other beverages and yogurt. Moreover, food products produced with the additive composition will be more nutritious and healthful than products which do not contain the additive. Products with the additive of the invention will have a higher fiber content, and also include vitamins and minerals which are present in the by-product from which the additive is made.
- the present invention provides a high fiber additive composition which is a by-product of milling processes wherein the high fiber additive enhances the fiber content of a variety of products including flour, yogurts, beverages, baking items, snack foods such as pretzels, cereal products such as breakfast cereals, and salsa.
- the additive is provided from a high fiber, low starch source of plant material.
- the source of high fiber, low starch is cereal bran or a mixture of bran obtained from the commercial dry milling of corn, wheat, barley, oats, rice, rye, sorghum or any other cereal grain.
- the high fiber, low starch source may be soy hulls.
- the low levels of starch in the additive composition makes it less sticky than additives with higher levels of starch, and hence, the additive composition of the invention can be used in a wide variety of food products.
- the high fiber additive composition comprises aspirated cereal bran having less than about 15 weight percent starch, which starch content is gelatinized, at least about 2 weight percent protein, and at least about 75 weight percent total dietary fiber.
- the starch in the cereal bran has been substantially gelatinized.
- the starch in the cereal bran is gelatinized by cooking it with at least about 0.05 weight percent, based upon the weight of the bran, calcium oxide or lime or equivalent thereof. This should provide the additive with at least about 0.025 weight percent calcium, based upon the weight of the additive.
- the additive should also provide a pH of at least about 7 when it is mixed with water and the additive comprises about 10 weight percent of the additive/water mixture.
- the high fiber additive composition comprises soy hulls having a very low starch content and at least about 2 weight percent protein, and at least about 75 weight percent total dietary fiber.
- the additive composition comprises soy hulls having little or no starch.
- the soy hulls also comprise at least about 2 weight percent protein and at least 75 weight percent dietary fiber.
- the soy hulls are heat treated under the same conditions used to gelatinize the starch in cereal bran. This heat treatment opens the structure of non starch polysaccarides such as arakinoxylans, beta glucans and pectic substances.
- the invention also includes a process for making the additive composition.
- the method comprises mixing aspirated cereal bran comprising less than about 15 weight percent starch or soy hulls with water or an alkaline agent and water to provide an aqueous fiber mixture and cooking the aqueous fiber mixture (or alkaline aqueous mixture) to gelatinize the starch in the cereal bran or open the polysaccharide structure in the soy hulls and provide a cooked bran or soy hulls.
- the cooked product is dried. If an alkaline agent is used during cooking, the cooked product is dried without first removing aqueous alkaline water, such as lime water, to provide a dried alkaline-treated bran.
- the water treated or alkaline treated bran is milled to a particle size, such that it will pass through a screen mesh with openings of not greater than 0.1 square mm.
- the high fiber additive is pulverized such that at least 70 weight percent of the material is smaller than 500 microns.
- the bran is corn bran
- the starch is corn starch
- the bran additive composition comprises aspirated bran having less than about 15 weight percent starch, of which at least about a substantial amount has been gelatinized.
- the alkaline agent, such as lime comprises from about 0.05 to about 5 weight percent based upon the weight of the by-product or bran. The amount of lime, water and cooking are effective for gelatinizing the starch. DETAILED DESCRIPTION OF THE INVENTION
- the present invention provides a high fiber additive composition which is made from a cereal grain by-product or soy hulls.
- the additive enhances nutritional value by increasing the fiber content of food products that it is added to.
- the additive composition comprises cereal grain by-product and gelatinized edible starch, at least about 2 weight percent protein, and from about 75 to about 90 weight percent total dietary fiber.
- the fiber can be measured as crude fiber, as neutral dietary fiber or as acid dietary fiber by known methods) .
- the by-product used to make the additive comprises from about 2 to less than about 15 weight percent starch and is preferably from about 5 to about 12 weight percent, with from about 7 to about 10 weight percent being most preferred.
- the starch in the additive which is made from cereal bran is substantially gelatinized to at least about 100% (i.e., with no native starch remaining).
- the greater percent of starch will be gelatinized (probably 100%).
- slightly less than 100 weight percent of the starch may be gelatinized.
- the degree to which the starch has been gelatinized may be determined by detecting the loss of birefringence in a manner known by those of skill in the art. For example, it may be determined by microscopic techniques, the absorption, cold paste viscosity, hot paste viscosity and cold water solubles methods described in U.S. Patent No. 3,404,986.
- the cereal by-product used to make the additive composition of the present invention may be an aspirated bran obtained from the commercial dry milling of wheat, barley, oats, rice, rye, sorghum or any other cereal or other grain.
- the aspirated bran is from the dry milling of whole corn of any type (dent, flint, sweet, pop, hybrid, yellow, white, blue, black, red, etc.) and, more preferably, is obtained from the dry milling of yellow and white corn.
- the dry aspirated bran has from about 10 to about 25 weight percent moisture.
- the bran may also be the white or other fiber produced by commercial wet milling of corn or other cereal grains. Different sizes of whole bran, and/or fragments or pieces of the whole bran, may be employed for the bran.
- the cereal bran by-product also contains at least about 2 weight percent protein.
- This protein may be from the class of albumins, globulins, prolamines or glutelins, for example, zein or glutelin, and adds flavor (good taste) to the products produced with the bran composition additive of the invention.
- the additive of the present invention may, optionally, contain one or more additional ingredients, such as vitamins (vitamins A, B, C, D, E, etc.), minerals (calcium, phosphorous, sulphur, magnesium, potassium, iron, zinc, manganese, etc.), germ, other carbohydrates, fats or oils, other proteinaceous materials (such as corn protein or wheat protein) , germ other nutrients, flavor ingredients, emulsifiers, preservatives, gums and/or like ingredients which may enhance the quality of products produced from the additive.
- vitamins vitamins A, B, C, D, E, etc.
- minerals calcium, phosphorous, sulphur, magnesium, potassium, iron, zinc, manganese, etc.
- germ other carbohydrates, fats or oils
- other proteinaceous materials such as corn protein or wheat protein
- germ other nutrients such as corn protein or wheat protein
- emulsifiers such as corn protein or wheat protein
- the quantities of these ingredients should be at a weight percent which is high enough to impart some additional beneficial property to products produced with the additive, but which are not so high as to detrimentally affect the increase in flexibility and/or stability imparted to these products by the by-product and gelatinized starch.
- the high fiber additive composition may be made by heating the cereal bran with water to gelatinize the starch in the bran or by heating the soy hulls in water to alter the non starch polysaccarides as describe above.
- the cereal bran or soy hulls may be the heated with an aqueous alkaline system if the ultimate application for the additive requires a lime constituent such as Mexican food where a lime taste is desirable.
- alkaline agent such as lime (CaO)
- water are mixed and are cooked to provide the additive composition.
- the water and alkaline agent are in amounts effective to gelatinize the edible starch in the cereal bran or open the polysaccharide structure of the polysaccarides in the soy hulls. at cooking temperatures of from about 70 to about 100°C.
- aspirated cereal bran is mixed with water and an alkaline agent, such as lime, to provide an aqueous alkaline bran mixture.
- the aqueous alkaline bran mixture contains from about 0.05 to about 5 weight percent lime based upon the weight percent of the byproduct used to prepare the additive, and preferably about 1.2 weight percent lime.
- the amount of alkaline agent in the aqueous alkaline bran mixture is effective for providing the mixture with a pH of from about 7 to about 11 and preferably to about 9.
- the water in the aqueous mixture is an amount effective for providing the cooked, lime-treated bran with a moisture content of from about 20 to about 85 weight percent.
- the amount of water used to achieve the latter moisture content is minimized so that an alkaline waste water stream is minimized or eliminated.
- Moisture may be provided to the cooked product by supplying steam for cooking the product. Steam also minimizes water used in the process and avoids a waste water stream.
- the moisture content of the cooked mixture will preferably be about 55 weight percent.
- the alkaline agent employed in the process is lime (calcium oxide) .
- the alkaline agent is preferably in a dry form.
- the lime can be added in the water employed to cook the cereal bran and starch, can be mixed with the bran and starch prior to water addition, or can be mixed with the bran and starch after water addition.
- the method for adding the lime to the bran and starch is not critical. However, liquid water is employed to cook the bran and starch. In a preferred cooking process, about 1.0 weight percent of dry lime is added to the aspirated cereal bran through a dry lime feeder and is mixed with the aspirated bran. Thereafter, water heated to about 200°F (93°C) is added into the cooker with mixing in a ratio of about 1 part of water or more to about 1 part of aspirated bran and lime mixture. This should result in a moisture content of the mixture of from about 50 to about 60 weight percent, which is optimal. However, moisture levels within the range of from about 20 to about 80 weight percent will work.
- a temperature which is effective to gelatinize the starch to at least about 100%, should be reached. Because corn starch usually gelatinizes at about 160°F (71°C), the cooking temperature, or temperature of the heated water, will generally be at least about 135°F. The temperatures employed for cooking and drying the cereal grain bran and starch should not be so high that -lithe composition being cooked or dried becomes burned and, perhaps, loses its functional properties.
- the preferred cooking temperature, or temperature of the heated water will generally be from about 167°F (75°C) to about 212°F (100°C), and is more preferable from about 195°F (90°C) to about 210°F (99°C), with about 197°F (92°C) being most preferred.
- the heated water is added through the cooker, and the suspension is stirred to suspend the lime into the aspirated cereal bran and starch.
- the mixture is mixed at this temperature for from about 20 seconds to about 600 seconds, and preferably from about 60 to about 300 seconds.
- the temperature of the lime-treated bran and starch upon its discharge from the cooker will generally be from about 190°F (87°C) to about 195°F (90°C), and is preferably about 197°F (92°C).
- the moisture content of the lime-treated bran fraction and starch upon such discharge will generally be from about 50 to about 60 weight percent.
- the cooking of the by-product, water and alkaline agent can be done in a continuous, or in a batch, process.
- the heating can be achieved in a number of ways, such as by directly injecting live steam or heated water into the mixtures or by adding steam or heated water to maintain the above-described temperature for the mixtures
- the cooked, alkaline-treated high fiber by product optionally may be stored for a period of time prior to drying. However, it must be stored at a temperature which is high enough to prevent microbial spoilage.
- the cooked alkaline-treated bran may be used wet or may be flash dried (flash dehydrated) without washing to quickly reduce the moisture content thereof to less than about 10 weight percent, and preferably to less than about 3 to about 5 weight percent.
- flash dehydration high velocity hot air currents having a temperature of from about 350 °F to from about 390°F are generally employed for rapid dehydration.
- the total residence time of the composition within the flash dehydrator is generally from about 2 to about 15 seconds.
- the method of drying to provide the cooked, dehydrated additive is not critical.
- the inlet temperature of the flash dryer is about 650°F (343°C), and the outlet temperature of the flash dryer is about 220°F (104°C) .
- the cooked dehydrated additive composition is milled in, for example, a stone mill, disc mill, hammer mill, cylinder mill, wet mill or other mill, or otherwise size reduced, such that the average particle diameter of the milled cooked dehydrated additive composition is generally less than about 0.1 square mm. (i.e., the particles will pass through a screen having 0.1 square mm openings) and preferably about 99% of it.
- the average particle size of the milled dehydrated additive composition need only be small enough such that it may be added to flour or dough, and tortillas or related products may be made therefrom.
- a hammermill is employed.
- the resulting cooked, dehydrated and milled additive composition then is sifted to remove material coarser than that which will pass through about a U.S. No. 40 mesh sieve.
- the moisture content of the sifted product will generally be less than about 10 weight percent and will preferably be less than about 8 weight percent. However, the moisture content of the sifted product is not critical. It is possible to add wet additives of the invention to wet masa or other dough to produce the tortillas and related products. 3. Preparation of High Fiber Food Products
- the food products to which the high fiber additive may be added may be made by mixing the additive with the flour, dough, beverage or other product such that the resulting product has from about 0.1 to about 10 weight percent additive.
- the additives of the present invention may be added in wet or dry form to corn or other cereal grain lime-treated or non-lime treated flour or dough by one of several different methods.
- the additive in dry, powdered form may be mixed with dry corn or other cereal grain flour (nixtamalized or not nixtamalized) . Thereafter, the dry mixture may be added with water to form a dough from which tortillas or related products may be made.
- the additive in dry, powdered form or wet form or the corn or other cereal grain flour may be mixed with water. Then, the resulting water may be mixed with the remaining dry ingredient (corn or other cereal grain flour or bran composition additive in dry, powdered form) to form a dough from which tortillas or related products may be made.
- Dry powdered or wet additive may be added with a tortilla dough and thoroughly homogenized therewith.
- Tortillas or related products may then be made from this dough.
- a flour may be produced by mixing 97.5 weight percent of a corn (limed or non-limed) or other cereal grain flour, such as masa, with 2.5 weight percent of the additive of the present invention. This mixture may then be made into a dough by the simple addition of from about 1 to about 1.4 parts by weight of ambient temperature water with about 1 part by weight (dry basis) of the flour mixture together with kneading. Tortillas and related products may then be prepared from this dough in the manner described hereinbelow.
Abstract
Description
Claims
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE69825436T DE69825436T2 (en) | 1997-05-15 | 1998-05-15 | GROUND GRAIN ELEMENT PRODUCT AS ADDITIV TO THE ENTIRE GENERATION OF DIETAETIC FIBERS |
AU74885/98A AU7488598A (en) | 1997-05-15 | 1998-05-15 | Milled cereal by-product which is an additive for increasing total dietary fiber |
AT98922305T ATE272329T1 (en) | 1997-05-15 | 1998-05-15 | GROUND GRAIN BY-PRODUCT AS AN ADDITIVE TO INCREASE THE OVERALL DIETATIC FIBERS |
CA002289498A CA2289498C (en) | 1997-05-15 | 1998-05-15 | Milled cereal by-product which is an additive for increasing total dietary fiber |
US09/424,008 US6610349B1 (en) | 1998-05-15 | 1998-05-15 | Milled cereal by-product which is an additive for increasing total dietary fiber |
EP98922305A EP0981283B1 (en) | 1997-05-15 | 1998-05-15 | Milled cereal by-product which is an additive for increasing total dietary fiber |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/857,770 | 1997-05-15 | ||
US08/857,770 US6056990A (en) | 1997-05-15 | 1997-05-15 | Milled cereal by-product which is an additive for flour and dough |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1998051165A1 true WO1998051165A1 (en) | 1998-11-19 |
Family
ID=25326709
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1998/009620 WO1998051158A1 (en) | 1997-05-15 | 1998-05-12 | Milled cereal by-product which is an additive for flour and dough |
PCT/US1998/009913 WO1998051165A1 (en) | 1997-05-15 | 1998-05-15 | Milled cereal by-product which is an additive for increasing total dietary fiber |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1998/009620 WO1998051158A1 (en) | 1997-05-15 | 1998-05-12 | Milled cereal by-product which is an additive for flour and dough |
Country Status (10)
Country | Link |
---|---|
US (1) | US6056990A (en) |
EP (2) | EP0987949B1 (en) |
AR (1) | AR012705A1 (en) |
AT (2) | ATE375085T1 (en) |
AU (2) | AU7380198A (en) |
CA (2) | CA2289489C (en) |
DE (2) | DE69838547D1 (en) |
DK (1) | DK0987949T3 (en) |
ES (2) | ES2296333T3 (en) |
WO (2) | WO1998051158A1 (en) |
Families Citing this family (28)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6309688B1 (en) * | 1996-10-30 | 2001-10-30 | SáNCHEZ Y DE LA CAMARA FELIPE ALBERTO | Dietetic maize tortilla |
US6268008B1 (en) * | 1997-07-15 | 2001-07-31 | Sergio Alejandro Celorio Garrido | Composition of nixtamilized maize dough for the production of maize pancakes |
US6610349B1 (en) * | 1998-05-15 | 2003-08-26 | Cargill, Incorporated | Milled cereal by-product which is an additive for increasing total dietary fiber |
US20020150650A1 (en) * | 1998-09-17 | 2002-10-17 | Cupp Carolyn Jean | Dental diet for reducing tartar |
US6572910B2 (en) | 2000-05-27 | 2003-06-03 | The Procter & Gamble Co. | Process for making tortilla chips with controlled surface bubbling |
US6830767B2 (en) | 2000-05-27 | 2004-12-14 | The Procter & Gamble Co. | Method for constrain-frying snack pieces having intact surface features |
US6428828B1 (en) | 2000-08-22 | 2002-08-06 | The Board Of Regents Of The University Of Nebraska | Enzymatic process for nixtamalization of cereal grains |
DE10047498A1 (en) * | 2000-09-26 | 2002-04-18 | Bosch Gmbh Robert | Compact-type sparking plug for motor vehicles, has insulator element joined to housing by friction-locked joint aligned in radial direction |
US20030198725A1 (en) * | 2001-11-28 | 2003-10-23 | Cardenas Juan De Dios Figueroa | Nixtamalized corn and products thereof |
US20050053708A1 (en) | 2002-08-09 | 2005-03-10 | Mihalos Mihaelos N. | Production of thin, irregular chips with scalloped edges and surface bubbles |
US20040091596A1 (en) * | 2002-11-13 | 2004-05-13 | Steve Schellhaass | Food product and method of manufacture |
FR2863454B1 (en) * | 2003-12-12 | 2006-04-07 | Gervais Danone Sa | CEREAL PRODUCTS HAVING A STRONG ANTIOXIDANT POWDER |
US20070281064A1 (en) * | 2004-03-19 | 2007-12-06 | Ansui Xu | High Fiber, Reduced Effective Carbohydrate Corn-Based Food Formulations |
EP1732400A4 (en) * | 2004-03-19 | 2008-09-24 | Cargill Inc | High fiber, reduced effective carbohydrate corn-based food formulations |
US7220443B2 (en) * | 2005-02-10 | 2007-05-22 | Sabritas, S. De R.L. De C.V. | Method for making instant masa |
US7740895B2 (en) * | 2005-02-28 | 2010-06-22 | The Board Of Trustees Of The University Of Illinois | Nixtamalization process and products produced therefrom |
US7820220B2 (en) | 2005-04-08 | 2010-10-26 | Kraft Foods Global Brands Llc | Production of baked snack chips with irregular shape having notched edges |
US20070087101A1 (en) * | 2005-10-14 | 2007-04-19 | Gusek Todd W | Soy-fortified corn dough and tortillas |
US20090130249A1 (en) * | 2007-11-20 | 2009-05-21 | Cargill, Incorporated | Methods to deliver low-inclusion ingredients into an animal feed ration |
US8152358B2 (en) * | 2007-11-20 | 2012-04-10 | Cargill, Incorporated | System and apparatus to deliver low-inclusion feed ingredients into livestock ration |
US8110239B2 (en) * | 2008-05-22 | 2012-02-07 | Sabritas, S. De R.L. De C.V. | Quick corn nixtamalization process |
KR20110025057A (en) * | 2009-09-02 | 2011-03-09 | 산요덴키가부시키가이샤 | Automatic bread machine |
JP5418212B2 (en) * | 2009-12-25 | 2014-02-19 | 三洋電機株式会社 | Automatic bread machine |
PL222606B1 (en) * | 2012-08-16 | 2016-08-31 | Dijo Baking Horeca Service Spółka Z Ograniczoną Odpowiedzialnością | Method for making tortilla |
MX364621B (en) * | 2013-10-14 | 2019-05-03 | Leopoldo Castro Genera Roberto | Process for a depth thermal treatment in maize for producing high performance integral nixtamal and reactor for obtaining necessary conditions for the process. |
SG11202006789SA (en) * | 2018-03-07 | 2020-08-28 | Nestle Sa | Flavour composition |
US10912320B2 (en) * | 2018-08-17 | 2021-02-09 | Gruma S.A.B. De Cv | Water- and energy-saving systems and methods for producing lime-cooked masa |
WO2022098610A1 (en) * | 2020-11-03 | 2022-05-12 | Wenger Manufacturing Inc. | Tortilla-making process |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4594260A (en) * | 1984-09-21 | 1986-06-10 | Imit, A.C. | Process for producing nixtamalized corn flour |
US4996063A (en) * | 1989-06-30 | 1991-02-26 | The United States Of America, As Represented By The Secretary Of Agriculture | Method for making a soluble dietary fiber composition from oats |
Family Cites Families (34)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US31513A (en) * | 1861-02-19 | haasz | ||
US2704257A (en) * | 1952-10-01 | 1955-03-15 | Process Millers Inc | Method of producing corn tortilla flour |
US3035918A (en) * | 1959-06-01 | 1962-05-22 | Battalle Dev Corp | Process for treating food |
US3194664A (en) * | 1960-05-19 | 1965-07-13 | Frito Company | Method for continuously producing nixtamal |
US3212904A (en) * | 1963-02-04 | 1965-10-19 | Quaker Oats Co | Process for preparing a precooked corn flour |
US3404986A (en) * | 1966-07-18 | 1968-10-08 | Krause Milling Co | Process for manufacturing corn flour |
US3554772A (en) * | 1967-01-30 | 1971-01-12 | Borden Inc | Method of pasteurizing flour |
US3368902A (en) * | 1967-03-22 | 1968-02-13 | Isadore A. Berg | Corn chip |
US3655385A (en) * | 1970-06-08 | 1972-04-11 | Roberto Gonzalez Barrera | Tortilla and process using edible hydrophilic gum |
US3653915A (en) * | 1970-06-08 | 1972-04-04 | Manuel Jesus Rubio | Tortilla and process using mono-or diglyceride |
US3859452A (en) * | 1972-07-03 | 1975-01-07 | Fausto Celorio Mendoza | Method for obtaining nixtamalized flours |
US4329371A (en) * | 1976-10-04 | 1982-05-11 | Seven-H Corporation | Method of processing grain |
CH630242A5 (en) * | 1978-02-10 | 1982-06-15 | Donald Graham Glen | PROCESS AND INSTALLATION FOR CONTINUOUSLY WHITENING AND STERILIZING PIECE FOOD PRODUCTS. |
US4221340A (en) * | 1979-01-11 | 1980-09-09 | Beehive Machinery, Inc. | Method and apparatus for producing a masa product |
JPS59232051A (en) * | 1983-06-13 | 1984-12-26 | Nippon Shokuhin Kako Kk | Preparation of ingredient similar to an (bean jam) |
US4555409A (en) * | 1984-04-09 | 1985-11-26 | Hart Edwin R | Cereal processing |
US5652010A (en) * | 1984-12-14 | 1997-07-29 | Nabisco, Inc. | Production of masa corn-based products |
US4710386A (en) * | 1985-01-29 | 1987-12-01 | General Foods Corporation | All natural, ready-to-eat enzyme-saccharified cereal derived from whole cereal grain |
JPS61192253A (en) * | 1985-02-22 | 1986-08-26 | House Food Ind Co Ltd | Production of heat-treated granular solid food and apparatus therefor |
US4735811A (en) * | 1985-10-25 | 1988-04-05 | The Pillsbury Company | Tortilla and method of manufacture |
US4770891A (en) * | 1986-01-20 | 1988-09-13 | Willard Miles J | Method for preparing sheeted fried snack products |
US4844937A (en) * | 1987-04-13 | 1989-07-04 | J. R. Scott Milling Company | Method for making puffable food products from corn and products produced therefrom |
US4985269A (en) * | 1990-06-12 | 1991-01-15 | Borden, Inc. | Continuous extrusion for tortilla chip production |
AU9016291A (en) * | 1990-11-06 | 1992-05-26 | E.I. Du Pont De Nemours And Company | High fiber and low ash cereal fibers |
US5176931A (en) * | 1992-03-13 | 1993-01-05 | Wenger Manufacturing, Inc. | Preparation of masa flour |
US5296253A (en) * | 1992-05-28 | 1994-03-22 | Texas A&M University | Intermediate moisture legume and cereal food product and method of producing |
US5225224A (en) * | 1992-07-15 | 1993-07-06 | Vannortwick H Christian | Process for forming corn grit food products |
US5362511A (en) * | 1992-09-14 | 1994-11-08 | The Procter & Gamble Company | Method of production of extruded protein-containing cereal grain-based food products having improved qualities |
US5532013A (en) * | 1993-10-21 | 1996-07-02 | Centro De Investigacion Y De Estudios Avanzados Del I.P.N. | Method for the preparation of instant fresh corn dough or masa |
US5558886A (en) * | 1993-10-21 | 1996-09-24 | Centro De Investigacion Y De Estudios Avanzados Del I.P.N. | Extrusion apparatus for the preparation of instant fresh corn dough or masa |
US5558898A (en) * | 1994-09-20 | 1996-09-24 | Wenger Manufacturing Inc. | Continuous method of producing masa flour |
US5928701A (en) * | 1995-06-07 | 1999-07-27 | The Procter & Gamble Company | Process for making fat-free corn chips |
AU2128497A (en) * | 1996-02-20 | 1997-09-02 | Conagra, Inc. | Method for producing a masa flour |
US6025011A (en) * | 1997-06-09 | 2000-02-15 | J. R. Short Milling Company | Process for producing nixtamal and masa flour |
-
1997
- 1997-05-15 US US08/857,770 patent/US6056990A/en not_active Expired - Lifetime
-
1998
- 1998-05-12 DE DE69838547T patent/DE69838547D1/en not_active Expired - Lifetime
- 1998-05-12 DK DK98921125T patent/DK0987949T3/en active
- 1998-05-12 AT AT98921125T patent/ATE375085T1/en not_active IP Right Cessation
- 1998-05-12 AU AU73801/98A patent/AU7380198A/en not_active Abandoned
- 1998-05-12 EP EP98921125A patent/EP0987949B1/en not_active Expired - Lifetime
- 1998-05-12 ES ES98921125T patent/ES2296333T3/en not_active Expired - Lifetime
- 1998-05-12 CA CA002289489A patent/CA2289489C/en not_active Expired - Lifetime
- 1998-05-12 WO PCT/US1998/009620 patent/WO1998051158A1/en active IP Right Grant
- 1998-05-15 AU AU74885/98A patent/AU7488598A/en not_active Abandoned
- 1998-05-15 EP EP98922305A patent/EP0981283B1/en not_active Expired - Lifetime
- 1998-05-15 WO PCT/US1998/009913 patent/WO1998051165A1/en active IP Right Grant
- 1998-05-15 AR ARP980102267A patent/AR012705A1/en active IP Right Grant
- 1998-05-15 ES ES98922305T patent/ES2226130T3/en not_active Expired - Lifetime
- 1998-05-15 AT AT98922305T patent/ATE272329T1/en not_active IP Right Cessation
- 1998-05-15 DE DE69825436T patent/DE69825436T2/en not_active Expired - Lifetime
- 1998-05-15 CA CA002289498A patent/CA2289498C/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4594260A (en) * | 1984-09-21 | 1986-06-10 | Imit, A.C. | Process for producing nixtamalized corn flour |
US4996063A (en) * | 1989-06-30 | 1991-02-26 | The United States Of America, As Represented By The Secretary Of Agriculture | Method for making a soluble dietary fiber composition from oats |
Also Published As
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CA2289489C (en) | 2006-10-10 |
US6056990A (en) | 2000-05-02 |
CA2289498A1 (en) | 1998-11-19 |
CA2289489A1 (en) | 1998-11-19 |
EP0987949A1 (en) | 2000-03-29 |
AU7488598A (en) | 1998-12-08 |
EP0981283A1 (en) | 2000-03-01 |
EP0987949B1 (en) | 2007-10-10 |
AR012705A1 (en) | 2000-11-08 |
DE69825436D1 (en) | 2004-09-09 |
DE69825436T2 (en) | 2005-07-28 |
DE69838547D1 (en) | 2007-11-22 |
ES2226130T3 (en) | 2005-03-16 |
WO1998051158A1 (en) | 1998-11-19 |
EP0981283A4 (en) | 2000-09-20 |
AU7380198A (en) | 1998-12-08 |
DK0987949T3 (en) | 2008-02-11 |
CA2289498C (en) | 2009-04-28 |
ES2296333T3 (en) | 2008-04-16 |
ATE375085T1 (en) | 2007-10-15 |
EP0987949A4 (en) | 2000-09-20 |
EP0981283B1 (en) | 2004-08-04 |
ATE272329T1 (en) | 2004-08-15 |
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